EP2893278B1 - Exchanger element for a heat exchanger, heat exchanger comprising such an exchanger element and method for the production of such an exchanger element - Google Patents

Exchanger element for a heat exchanger, heat exchanger comprising such an exchanger element and method for the production of such an exchanger element Download PDF

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Publication number
EP2893278B1
EP2893278B1 EP13766603.8A EP13766603A EP2893278B1 EP 2893278 B1 EP2893278 B1 EP 2893278B1 EP 13766603 A EP13766603 A EP 13766603A EP 2893278 B1 EP2893278 B1 EP 2893278B1
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EP
European Patent Office
Prior art keywords
plate
ribs
exchanger
face
exchanger element
Prior art date
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Application number
EP13766603.8A
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German (de)
French (fr)
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EP2893278A2 (en
Inventor
Frédéric Crayssac
Marc Wagner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Publication of EP2893278A2 publication Critical patent/EP2893278A2/en
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0037—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23P—METAL-WORKING NOT OTHERWISE PROVIDED FOR; COMBINED OPERATIONS; UNIVERSAL MACHINE TOOLS
    • B23P15/00—Making specific metal objects by operations not covered by a single other subclass or a group in this subclass
    • B23P15/26—Making specific metal objects by operations not covered by a single other subclass or a group in this subclass heat exchangers or the like
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/4935—Heat exchanger or boiler making

Definitions

  • the present invention relates to a heat exchanger element according to the preamble of claim 1 for a heat exchanger for transferring heat from at least one primary fluid called caloric fluid to at least one secondary fluid called refrigerant.
  • the present invention relates to a heat exchanger, for a cryogenic gas separation unit, and comprising a plurality of exchanger elements according to the invention.
  • the present invention relates to a manufacturing method for manufacturing such an exchanger element.
  • Such an exchanger is known from the document US 1,662,870 .
  • the present invention finds particular application in the field of gas separation by cryogenics, in particular the separation of air by cryogenics (known by the acronym "ASU" for air separation unit) exploited for the production of oxygen gas under pressure.
  • ASU air separation unit
  • US6951245B1 describes a heat exchanger for transferring heat from a circulating fluid to a refrigerant.
  • the heat exchanger has a plurality of plates, ribs projecting from each plate, and closure bars extending around the plates.
  • the plates have the function of supporting the ribs and channeling fluid, calorigen or refrigerant.
  • the ribs function to form channels for the flow of fluid, heat or refrigerant.
  • the closing bars are used to close the channels.
  • the high pressure oxygen flow can cause direct ignition of the aluminum alloy on a hot spot created locally. by plastic deformation, solder fracture, particle impact, flow friction etc.
  • the risk of direct ignition increases with the service pressure.
  • the present invention aims to solve, in whole or in part, the problems mentioned above.
  • the plate, at least a portion of the ribs and at least a portion of the closure bars are made in one piece, therefore composed of one and the same material.
  • the components of the exchanger element are therefore integral, and they do not require or little solder.
  • such an exchanger element has a very high mechanical strength, which allows the heat exchanger to operate at caloric fluid and / or refrigerant pressures greater than 50 bar A, or even 80 bar A, or even at 100 bar A. Furthermore, as such a heat exchanger element comprises little or no solder, the risk of direct ignition is reduced in the case of air separation.
  • full means a plate which is solid, that is to say without cavities or cavities.
  • the plate, all the ribs and all the closing bars are monobloc.
  • US Patent 1662870 has an exchanger element according to the preamble of claim 1 but does not have distribution channels for a fluid exchange.
  • an exchanger element according to claim 1.
  • such an exchanger element has a particularly high mechanical strength, which allows the heat exchanger to operate under caloric fluid and / or refrigerant pressures greater than 50 bar A, or even 80 bar A, or even at 100 bar A.
  • the closure bars are arranged so that all the edges of the plate are bordered by at least one closing bar.
  • the heat exchanger is sealed on each of its edges by means of one-piece closure bars, therefore mechanically resistant.
  • the plate has generally the shape of a rectangle, the exchanger element having four closure bars extending respectively along the four edges of the plate.
  • the heat exchanger has plane faces formed by the stacking of the rectilinear edges of the plates. which simplifies its assembly with fluid inlet boxes and fluid outlet boxes.
  • only one face of the plate has ribs.
  • each rib is relatively large because the ribs of the exchange element are directly in contact with the plate of the superimposed exchange element.
  • the two faces of the plate comprise ribs.
  • Such an exchange element has a high rib density, and thus provides large areas for heat exchange.
  • the ribs of the first face are offset with respect to the ribs of the second face, the ribs preferably being uniformly distributed on each face.
  • the ribs of the first face are not located in line with the ribs of the second face.
  • the ribs have rectangular cross sections and are similar to each other.
  • grooves are of variable section according to the manufacturing mode (mechanical machining, rolling or chemical machining)
  • ribs have relatively simple shapes to achieve.
  • two consecutive ribs are spaced apart by a first pitch
  • two consecutive ribs are spaced apart by a second pitch which is greater than first step, preferably between 1 and 2 times the first step.
  • a lateral rib which is the rib closest to an edge of the plate, is spaced from the corresponding closing bar by approximately 1 times the pitch
  • the opposite lateral rib which is the rib closest to the opposite edge of the plate, is spaced from the corresponding closing bar by approximately twice the pitch.
  • the ribs of a first face of the plate have a first height
  • the ribs of the second face of the plate have a second height, the second height being different from the first height.
  • each rib has a width of between 0.3 mm and 1.6 mm, preferably between 0.4 mm and 1.5 mm, each rib has a height of between 0.8. mm and 2.7 mm, preferably between 1.0 mm and 2.5 mm, and the plate has a thickness of between 0.6 mm and 1.7 mm, preferably between 0.8 mm and 1.5 mm .
  • a rib width gives each rib a high mechanical strength, which in particular reduces the risk of ignition of aluminum, when a fluid is oxygen because the monobloc exchanger element can be manufactured with a larger rib width than in the prior art.
  • ribs have notches arranged so as to allow communication between consecutive channels.
  • such notches allow the flow of circulating fluid or refrigerant between two consecutive channels.
  • the ribs are arranged so that each channel has a width of between 0.8 mm and 1.2 mm.
  • each channel has a width of between 0.8 mm and 1.2 mm.
  • the material forming the plate, the ribs and the one-piece closure bars is selected from the group consisting of copper, copper alloys, a stainless steel, aluminum, aluminum alloys in particular of grade 3003, 3004, 3104 and 3005, plated brazing alloys 4004, 4104, 4343, 4045, 4047A and their combination with those of the 3000 family
  • the exchanger element comprises solder disposed on ribs and / or on at least one closure bar.
  • the exchanger element comprises solder disposed on a face of the plate without ribs, if any.
  • solder makes it possible to secure the exchanger elements in pairs.
  • ribs extend, projecting on at least one face of the plate, parallel to each other so as to form so-called exchange channel walls parallel to each other.
  • Such parallel exchange channels can circulate the circulating fluid or refrigerant with relatively low pressure losses and over most of the length of the plate.
  • the distribution channels extend at angles between 45 ° and 90 ° with respect to the exchange channels.
  • the hydraulic diameter of the distribution channels is greater than the hydraulic diameter of the exchange channels.
  • such hydraulic diameters facilitate the distribution of circulating fluid and refrigerant, because the pressure drop generated in the region of the exchange channels is greater than the pressure drop generated in each region of the distribution channels.
  • the hydraulic diameters can be variable according to the exchange channels supplied (chemically machined channels).
  • such a “hybrid” heat exchanger element has one side that only fulfills the heat exchange function, while the other side also performs a fluid distribution function.
  • the subject of the present invention is a heat exchanger, for a cryogenic gas separation unit, comprising several exchanger elements stacked and joined together, for example by means of solder, so that the plates extend parallel to each other, the heat exchanger being characterized in that it comprises several exchanger elements according to the invention, preferably all the exchanger elements are according to the invention.
  • such a heat exchanger has a very high mechanical strength, which allows it to operate under fluid pressures calorigenic and / or refrigerant greater than 50 bar A, or even 80 bar A, or even 100 bar A.
  • exchange-channel exchanger elements mentioned above are stacked alternately with the above-mentioned exchanger elements with distribution channels and exchange channels.
  • this heat exchanger comprises a stack of exchanger elements of which at least one in two has distribution channels.
  • an exchanger element according to the invention has a very high mechanical strength and has exchange channels and distribution channels.
  • the plate blank has a thickness greater than 1 mm.
  • a thickness makes it possible to manufacture a plate having a very high mechanical strength, because the plate is relatively thick.
  • the tool comprises at least two coaxial wheels and separated by a distance corresponding to a width of a rib, the rollers rolling against said at least one face of the blank plate.
  • the figure 1 illustrates a part of an exchanger element 1 adapted to compose a heat exchanger for transferring heat from at least one primary fluid called caloric fluid to at least one secondary fluid called refrigerant.
  • the exchanger element 1 comprises a plate 2, ribs 4 and closing bars 8.1 and 8.3.
  • the plate 2, the ribs 4 and the closing bars 8.1 and 8.3 are monobloc.
  • the plate 2, all the ribs 4 and all the closing bars 8.1 and 8.3 are monobloc.
  • the ribs are also called "fins”.
  • the plate is also called "base”.
  • the plate 2, the ribs 4 and the closing bars 8.1 and 8.3 are made in one piece, and therefore composed of a single material.
  • the material forming the one-piece assembly composed of the plate 2, the ribs 4 and the closing bars 8.1 and 8.3 is here an aluminum alloy of grade 3003.
  • the plate 2 is full, flat and generally has the shape of a rectangle.
  • the edges of the plate 2 extend respectively in a longitudinal direction X2 and a lateral direction Y2.
  • the ribs 4 extend here projecting on one side of the plate 2.
  • the opposite face 2.1 is devoid of ribs.
  • Each rib 4 forms a portion of a wall of a respective channel 6.
  • the ribs here have cross sections, in a plane perpendicular to the longitudinal direction X2, which are rectangular and similar to each other.
  • Each channel 6 is adapted for the flow of circulating fluid or refrigerant. As the ribs 4 extend parallel to each other and to the longitudinal direction X2, the channels 6 are parallel to each other and to the longitudinal direction X2.
  • Each channel 6 is delimited by a rib 4 of the exchanger element 1, by a rib of the adjacent exchanger element and by the plate 2, which defines the "bottom" of the channel 6.
  • each channel 6 channels the circulating fluid or refrigerant, depending on whether it is supplied with circulating fluid or refrigerant.
  • the channels 6 are called exchange channels, since they contribute to fulfilling the function of heat transfer between the circulating fluid and the refrigerant via, in particular, the plate 2.
  • the exchanger element 1 comprises two closing bars 8.1 and 8.3.
  • the closing bars 8.1 and 8.3 extend respectively along two edges of the plate 2.
  • the closing bars 8.1 and 8.3 extend parallel to the longitudinal direction X2.
  • the closure bars 8.1 and 8.3 extend along the edges of the plate 2 so as to close the channels 6.
  • the closing bars 8.1, and 8.3 line, thus close respectively a channel 6 located near a lateral edge of the plate 2.
  • the closing bars 8.1 and 8.3 are here arranged so that all the edges of the plate 2 are bordered by a respective closing bar 8.1 and 8.3.
  • each edge of the plate 2 may be bordered by several separate closing bars.
  • at least one edge of the plate may have a portion of its length which is not bordered by a closing bar.
  • each closure bar may comprise an opening, usually called “window”, for introducing or discharging fluid respectively into or out of the channels.
  • the plate 2 has a thickness E2 of about 1.2 mm.
  • Each rib 4 has a width W4 of about 0.5 mm and a height H4 of about 1.8 mm.
  • Each channel 6 has a width W6 of about 1.0 mm.
  • the plate 2 has a length L2 of about 6 m measured in the longitudinal direction X2.
  • the plate 2 has a width W2 of about 2.5 m, measured in the transverse direction Y2.
  • the exchanger element 1 comprises solder disposed on the ribs 4 and on the closing bars 8.1 and 8.3. This solder forms a layer about 0.1 mm thick.
  • the exchanger element 1 comprises solder disposed on the face 2.1 of the plate 2, that is to say the face without ribs.
  • the figure 3 illustrates an exchanger element 101 according to the invention.
  • the description of the exchanger element 1 given above in relation to the Figures 1 and 2 can be transposed to the exchanger element 101, with the exception of the notable differences set out below.
  • a component of the exchanger element 101 which is identical or corresponding, in structure or function, to a component of the exchanger element 1 has the same numerical reference increased by 100.
  • a plate 102 is defined.
  • ribs 104 defining exchange channels 106, as well as closing bars 108.1, 108.2, 108.3 and 108.4.
  • the exchanger element 101 differs from the exchanger element 1, in particular since the exchanger element 101 has ribs 105 which are arranged, projecting on one face of the plate 102, so as to form walls.
  • second channels said distribution channels 107, so that the distribution channels 107 extend transversely to the exchange channels 106. As shown in FIG. figure 3 the distribution channels 107 extend at angles of about 90 ° to the exchange channels 106.
  • the arrangement of the ribs 105 makes it possible to favor the distribution of circulating fluid or refrigerant, since the pressure drop generated in the region of the exchange channels 106 is greater than the pressure drop generated in each region of the distribution channels. .
  • the exchanger element 101 differs from the exchanger element 1, because the exchanger element 101 has four closing bars 108.1, 108.2, 108.3, 108.4 which extend respectively along the four edges. of the plate 102.
  • the closing bars 108.1, 108.2, 108.3, 108.4 are parallel in pairs.
  • the figure 4 illustrates an exchanger element 201 according to the invention.
  • the description of the exchanger element 101 given above in relation to the figure 3 may be transposed to the exchanger element 201, with the exception of the notable differences set out below.
  • a component of the exchanger element 201 which is identical or corresponding, in structure or function, to a component of the exchanger element 101 has the same numerical reference increased by 100.
  • the exchanger element 201 differs from the exchanger element 101, in particular because the exchanger element 201 has ribs 205 which are arranged, projecting on one face of the plate 202, so as to form walls distribution channels 207, so that the distribution channels 207 extend obliquely to the exchange channels 206. As shown in FIG. figure 4 , the distribution channels 207 extend at angles of approximately 45 ° with respect to the exchange channels 206.
  • the arrangement of the ribs 205 makes it possible to give greater priority to the distribution of circulating fluid or refrigerant, since the pressure drop generated in the region of the exchange channels 206 is greater than the pressure drop generated in each region of the distribution channels. 207.
  • a heat exchanger according to the invention also comprises unrepresented feed boxes which are secured, for example by welding, on external faces. of the heat exchanger.
  • feed boxes allow the entry or exit of circulating fluid or refrigerant in or out of the distribution channels 107 or 207, so in or out of the exchange channels 106 or 206.
  • the feed boxes can be arranged on the longitudinal end portions of the exchanger element 101 or 201, so that these feed boxes are fluidly connected to the passages defined by all of the distribution channels 107 or 207.
  • the figure 5 illustrates a heat exchanger 300 for composing a unit not shown cryogenic gas separation.
  • the heat exchanger 300 comprises several exchanger elements 301, 321, 341 and so on. according to the invention, which are stacked and joined together by means of solder.
  • a component of the exchanger element 301, 321 or 341 identical or corresponding, by its structure or function, to a component of the exchanger element 1 or 101 has the same numerical reference increased by 100 or 200.
  • plates 302, 322, 342, exchange channels 306, 326, 346 and closing bars 308, 328, 348 are defined.
  • the figure 5 illustrates a cross-section in a plane perpendicular to the longitudinal direction and passing through the middle region of the exchanger elements 301, 321 or 341, i.e. a region having only exchange channels 306, 326 and 346
  • the plates 302, 322, 342 extend parallel to one another.
  • the heat exchanger element 301, 321 or 341 differs from the heat exchanger element 101, in particular because the heat exchanger element 301, 321 or 341 has ribs which protrude on both sides of the plate. respective 302, 322 or 342.
  • the exchanger element 301 has ribs 304.1 on a first face and ribs 304.2 on its second face.
  • the exchanger element 321 has ribs 324.1 on a first face and ribs 324.2 on its second face, and the exchanger element 341 has ribs 344.1 on one face and ribs 344.2 on its second face. face.
  • the exchanger element 301, 321 or 341 differs from the exchanger element 101, since the first face of the plate 302, 322 or 342 has ribs forming walls of parallel exchange channels 306. While the second face of the plate 302, 322 or 342 comprises, on the one hand, ribs 304.2, 324.1 forming walls of exchange channels 326 and, on the other hand, ribs not shown forming walls of distribution channels that are transverse to exchange channels 326 such as distribution channels 207.
  • the heat exchanger 300 comprises a stack of heat exchanger elements 301, 321, 341 of which one in two has distribution channels similar to the distribution channels 207.
  • the exchanger element 301, 321 or 341 is "hybrid" because it only has exchange channels on one side, and exchange channels plus distribution channels on the opposite side .
  • the heat exchanger may comprise exchanger elements with exchange channels which are stacked alternately with exchanger elements with distribution channels.
  • the ribs 304.1, 324.1 or 344.1 of the first face are offset with respect to the respective ribs 304.2, 324.2 or 344.2 of the second face.
  • the ribs 304.1, 324.1 or 344.1 of the first face are not located in line with the respective ribs 304.2, 324.2 or 344.2 of the second face.
  • two consecutive ribs 304.1 are spaced apart by a first pitch P304.1
  • two consecutive ribs 304.2 are spaced apart by a second pitch P304.2 which is greater than the first step P304.1.
  • the second step P304.2 is 1.5 times the first step.
  • the channels 306 and 326, after stacking of the exchanger elements 301 and 321, have different widths.
  • the lateral rib 304.1 which is the rib closest to the left edge of the plate 301 is spaced from the corresponding closing bar 308 by approximately 1 times the pitch P304.1.
  • the step of plastic deformation of the plate blank is performed by moving the material, but without removing material.
  • the plate blank has a thickness of about 2 mm.
  • the tool comprises at least two coaxial wheels and separated by a distance corresponding to a width W4 of a rib 4.
  • the unrepresented rollers move in rotation against the face of the plate blank. All the ribs 4 are thus made.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Description

La présente invention concerne un élément d'échangeur conforme au préambule de la revendication 1 pour un échangeur de chaleur destiné à transférer de la chaleur d'au moins un fluide primaire dit fluide calorigène vers au moins un fluide secondaire dit fluide frigorigène. De plus, la présente invention concerne un échangeur de chaleur, pour une unité de séparation de gaz par cryogénie, et comprenant plusieurs éléments d'échangeur selon l'invention. Par ailleurs, la présente invention concerne un procédé de fabrication pour fabriquer un tel élément d'échangeur. Un tel échangeur est connu du document US 1,662,870 .The present invention relates to a heat exchanger element according to the preamble of claim 1 for a heat exchanger for transferring heat from at least one primary fluid called caloric fluid to at least one secondary fluid called refrigerant. In addition, the present invention relates to a heat exchanger, for a cryogenic gas separation unit, and comprising a plurality of exchanger elements according to the invention. Furthermore, the present invention relates to a manufacturing method for manufacturing such an exchanger element. Such an exchanger is known from the document US 1,662,870 .

La présente invention trouve notamment application dans le domaine de la séparation de gaz par cryogénie, en particulier de la séparation d'air par cryogénie (connue sous l'acronyme anglais « ASU » pour unité de séparation d'air) exploitée pour la production d'oxygène gazeux sous pression.The present invention finds particular application in the field of gas separation by cryogenics, in particular the separation of air by cryogenics (known by the acronym "ASU" for air separation unit) exploited for the production of oxygen gas under pressure.

US6951245B1 décrit un échangeur de chaleur pour transférer de la chaleur d'un fluide calorigène vers un fluide frigorigène. L'échangeur de chaleur comporte plusieurs plaques, des nervures s'étendant en saillie sur chaque plaque, ainsi que des barres de fermeture s'étendant autour des plaques. US6951245B1 describes a heat exchanger for transferring heat from a circulating fluid to a refrigerant. The heat exchanger has a plurality of plates, ribs projecting from each plate, and closure bars extending around the plates.

Les plaques ont pour fonction de supporter les nervures et de canaliser du fluide, calorigène ou frigorigène. Les nervures ont pour fonction de former des canaux pour l'écoulement de fluide, calorigène ou frigorigène. Les barres de fermeture périphériques ont pour fonction d'obturer les canaux.The plates have the function of supporting the ribs and channeling fluid, calorigen or refrigerant. The ribs function to form channels for the flow of fluid, heat or refrigerant. The closing bars are used to close the channels.

Dans l'échangeur de chaleur d' US6951245B1 , les plaques, les nervures et les barres de fermeture sont solidarisées entre elles au moyen de brasure. En d'autres termes, les nervures et les barres de fermeture sont brasées sur les plaques.In the heat exchanger US6951245B1 the plates, the ribs and the closure bars are joined together by means of brazing. In other words, the ribs and closure bars are brazed to the plates.

Cependant, un tel échangeur de chaleur de l'art antérieur présente des risques de défauts de fabrication, car il est difficile de maîtriser le procédé de brasage. En particulier, certaines brasures pourraient être défectueuses. De tels défauts de fabrication entraînent des risques de défaillance de l'échangeur de chaleur. Ces risques de défaillance augmentent avec la pression de service prévue pour les fluides. Pour certaines applications, les fluides peuvent atteindre une pression comprise entre 50 bars et 100 bars.However, such a heat exchanger of the prior art has the risk of manufacturing defects, because it is difficult to control the brazing process. In particular, some solders could be defective. Such manufacturing defects lead to the risk of failure of the heat exchanger. These risks of failure increase with the expected working pressure for the fluids. For certain applications, the fluids can reach a pressure of between 50 bars and 100 bars.

En outre, lors de la séparation d'air par cryogénie dans un échangeur de chaleur en alliage d'aluminium, l'écoulement d'oxygène sous haute pression peut causer une inflammation directe de l'alliage d'aluminium sur un point chaud créé localement par une déformation plastique, une rupture de brasure, un impact de particules, des frottements d'écoulement etc. Or, le risque d'inflammation directe augmente avec la pression de service.In addition, when air is cryogenically separated in an aluminum alloy heat exchanger, the high pressure oxygen flow can cause direct ignition of the aluminum alloy on a hot spot created locally. by plastic deformation, solder fracture, particle impact, flow friction etc. However, the risk of direct ignition increases with the service pressure.

La présente invention vise notamment à résoudre, en tout ou partie, les problèmes mentionnés ci-avant.The present invention aims to solve, in whole or in part, the problems mentioned above.

À cet effet, l'invention a pour objet un élément d'échangeur, pour échangeur de chaleur destiné à transférer de la chaleur d'au moins un fluide primaire dit fluide calorigène vers au moins un fluide secondaire dit fluide frigorigène, l'élément d'échangeur comportant :

  • au moins une plaque qui est pleine ;
  • des nervures qui s'étendent en saillie sur au moins une face de la plaque, chaque nervure formant au moins une portion d'une paroi d'un canal respectif adapté pour l'écoulement de fluide calorigène ou de fluide frigorigène ; et
  • des barres de fermeture s'étendant suivant des bords de la plaque de façon à obturer au moins une partie des canaux ;
l'élément d'échangeur étant caractérisé en ce que la plaque, au moins une partie des nervures et au moins une partie des barres de fermeture sont monoblocs.For this purpose, the subject of the invention is an exchanger element, for a heat exchanger intended to transfer heat from at least one primary fluid called a heat transfer fluid to at least one secondary fluid called refrigerant, the element exchanger comprising:
  • at least one plate that is full;
  • ribs projecting from at least one face of the plate, each rib forming at least a portion of a wall of a respective channel adapted for the flow of circulating fluid or refrigerant; and
  • closure bars extending along edges of the plate so as to seal at least a portion of the channels;
the exchanger element being characterized in that the plate, at least a portion of the ribs and at least a portion of the closure bars are monobloc.

En d'autres termes, la plaque, au moins une partie des nervures et au moins une partie des barres de fermeture sont réalisées en une seule pièce, donc composées d'un seul et même matériau. Les composants de l'élément d'échangeur sont donc solidaires, et ils ne nécessitent pas ou peu de brasure.In other words, the plate, at least a portion of the ribs and at least a portion of the closure bars are made in one piece, therefore composed of one and the same material. The components of the exchanger element are therefore integral, and they do not require or little solder.

Ainsi, un tel élément d'échangeur présente une résistance mécanique très élevée, ce qui permet à l'échangeur de chaleur de fonctionner sous des pressions de fluide calorigène et/ou frigorigène supérieures à 50 bar A, voire à 80 bar A, voire même à 100 bar A. En outre, comme un tel élément d'échangeur comprend peu ou pas de brasures, le risque d'inflammation directe est réduit dans le cas de la séparation d'air.Thus, such an exchanger element has a very high mechanical strength, which allows the heat exchanger to operate at caloric fluid and / or refrigerant pressures greater than 50 bar A, or even 80 bar A, or even at 100 bar A. Furthermore, as such a heat exchanger element comprises little or no solder, the risk of direct ignition is reduced in the case of air separation.

Dans la présente demande, le terme « pleine » désigne une plaque qui est massive, c'est-à-dire dépourvue de creux ou de cavités.In the present application, the term "full" means a plate which is solid, that is to say without cavities or cavities.

Selon l'invention, la plaque, toutes les nervures et toutes les barres de fermeture sont monoblocs.According to the invention, the plate, all the ribs and all the closing bars are monobloc.

US-A-1662870 présente un élément d'échangeur selon le préambule de la revendication 1 mais ne présente pas de canaux de distribution permettant un échange de fluides. US Patent 1662870 has an exchanger element according to the preamble of claim 1 but does not have distribution channels for a fluid exchange.

Selon un objet de l'invention, il est prévu un élément d'échangeur selon la revendication 1.According to one object of the invention, there is provided an exchanger element according to claim 1.

Ainsi, un tel élément d'échangeur présente une résistance mécanique particulièrement élevée, ce qui permet à l'échangeur de chaleur de fonctionner sous des pressions de fluide calorigène et/ou frigorigène supérieures à 50 bar A, voire à 80 bar A, voire même à 100 bar A.Thus, such an exchanger element has a particularly high mechanical strength, which allows the heat exchanger to operate under caloric fluid and / or refrigerant pressures greater than 50 bar A, or even 80 bar A, or even at 100 bar A.

Selon une variante du mode de réalisation précédent, les barres de fermeture sont agencées de sorte que tous les bords de la plaque sont longés par au moins une barre de fermeture. Ainsi, l'échangeur de chaleur est étanche sur chacun de ses bords au moyen de barres de fermeture monoblocs, donc mécaniquement résistantes.According to a variant of the previous embodiment, the closure bars are arranged so that all the edges of the plate are bordered by at least one closing bar. Thus, the heat exchanger is sealed on each of its edges by means of one-piece closure bars, therefore mechanically resistant.

Selon un mode de réalisation de l'invention, la plaque a globalement la forme d'un rectangle, l'élément d'échangeur comportant quatre barres de fermeture s'étendant respectivement le long des quatre bords de la plaque.According to one embodiment of the invention, the plate has generally the shape of a rectangle, the exchanger element having four closure bars extending respectively along the four edges of the plate.

Ainsi, avec des plaques rectangulaires, l'échangeur de chaleur présente des faces planes formées par l'empilement des bords rectilignes des plaques, ce qui simplifie son assemblage avec des boîtes d'entrée de fluides et des boîtes de sortie de fluides.Thus, with rectangular plates, the heat exchanger has plane faces formed by the stacking of the rectilinear edges of the plates. which simplifies its assembly with fluid inlet boxes and fluid outlet boxes.

Selon un mode de réalisation de l'invention, une seule face de la plaque comporte des nervures.According to one embodiment of the invention, only one face of the plate has ribs.

Ainsi, la tolérance de fabrication de chaque nervure est relativement grande, car les nervures de l'élément d'échange sont directement en contact avec la plaque de l'élément d'échange superposé.Thus, the manufacturing tolerance of each rib is relatively large because the ribs of the exchange element are directly in contact with the plate of the superimposed exchange element.

Selon un mode de réalisation de l'invention, les deux faces de la plaque comportent des nervures.According to one embodiment of the invention, the two faces of the plate comprise ribs.

Ainsi, un tel élément d'échange a une densité de nervures élevée, et il offre donc de grandes surfaces pour l'échange de chaleur.Thus, such an exchange element has a high rib density, and thus provides large areas for heat exchange.

Selon une forme de réalisation du mode de réalisation précédent, les nervures de la première face sont décalées par rapport aux nervures de la deuxième face, les nervures étant de préférence uniformément répartis sur chaque face.According to an embodiment of the preceding embodiment, the ribs of the first face are offset with respect to the ribs of the second face, the ribs preferably being uniformly distributed on each face.

En d'autres termes, les nervures de la première face ne sont pas situées au droit des nervures de la deuxième face.In other words, the ribs of the first face are not located in line with the ribs of the second face.

Ainsi, un tel agencement décalé des nervures permet d'atteindre une densité très élevée de nervures dans l'échangeur de chaleur. En effet, deux éléments d'échangeur consécutifs peuvent être superposés avec leurs nervures respectives distantes, ce qui forme de nombreux canaux.Thus, such an offset arrangement of the ribs makes it possible to achieve a very high density of ribs in the heat exchanger. Indeed, two consecutive exchanger elements can be superimposed with their respective respective ribs, which forms many channels.

Selon une variante de l'invention, les nervures ont des sections transversales rectangulaires et semblables entre elles.According to a variant of the invention, the ribs have rectangular cross sections and are similar to each other.

Selon une variante de l'invention, des rainures sont de section variable suivant le mode fabrication (usinage mécanique, roulage ou usinage chimique )According to a variant of the invention, grooves are of variable section according to the manufacturing mode (mechanical machining, rolling or chemical machining)

Ainsi, de telles nervures ont des formes relativement simples à réaliser. Selon une variante de l'invention, sur une première face de la plaque, deux nervures consécutives sont distantes d'un premier pas, et sur une deuxième face de la plaque, deux nervures consécutives sont distantes d'un deuxième pas qui est supérieur au premier pas, de préférence compris entre 1 fois et 2 fois le premier pas. Ainsi, de telles nervures permettent de former des canaux, par empilement des éléments d'échangeur, qui ont des largeurs différentes, suivant la nature, le débit et/ou la pression du fluide à canaliser.Thus, such ribs have relatively simple shapes to achieve. According to a variant of the invention, on a first face of the plate, two consecutive ribs are spaced apart by a first pitch, and on a second face of the plate, two consecutive ribs are spaced apart by a second pitch which is greater than first step, preferably between 1 and 2 times the first step. Thus, such ribs make it possible to form channels, by stacking the exchanger elements, which have different widths, depending on the nature, the flow rate and / or the pressure of the fluid to be channeled.

Selon une variante de l'invention, sur chaque face de la plaque, une nervure latérale, qui est la nervure la plus proche d'un bord de la plaque, est distante de la barre de fermeture correspondante d'environ 1 fois le pas, et la nervure latérale opposée, qui est la nervure la plus proche du bord opposé de la plaque, est distante de la barre de fermeture correspondante d'environ 2 fois le pas. Ainsi, on peut alterner un élément d'échangeur tourné vers le haut avec un élément d'échangeur identique tourné vers le bas, ce qui permet de former des canaux de largeurs différentes entre les deux faces de la plaque.According to a variant of the invention, on each face of the plate, a lateral rib, which is the rib closest to an edge of the plate, is spaced from the corresponding closing bar by approximately 1 times the pitch, and the opposite lateral rib, which is the rib closest to the opposite edge of the plate, is spaced from the corresponding closing bar by approximately twice the pitch. Thus, it is possible to alternate an exchanger element facing upwards with an identical exchanger element facing downwards, which makes it possible to form channels of different widths between the two faces of the plate.

Selon une variante de l'invention, les nervures d'une première face de la plaque ont une première hauteur, les nervures de la deuxième face de la plaque ont une deuxième hauteur, la deuxième hauteur étant différente de la première hauteur. Ainsi, on peut adapter les nervures en fonction de la nature, le débit et/ou la pression d'un premier fluide et d'un deuxième fluide à canaliser.According to a variant of the invention, the ribs of a first face of the plate have a first height, the ribs of the second face of the plate have a second height, the second height being different from the first height. Thus, one can adapt the ribs depending on the nature, flow and / or pressure of a first fluid and a second fluid to channel.

Selon un mode de réalisation de l'invention, chaque nervure a une largeur comprise entre 0,3 mm et 1,6 mm, de préférence entre 0,4 mm et 1,5 mm, chaque nervure a une hauteur comprise entre 0,8 mm et 2,7 mm, de préférence entre 1,0 mm et 2,5 mm, et la plaque a une épaisseur comprise entre 0,6 mm et 1,7 mm, de préférence entre 0,8 mm et 1,5 mm.According to one embodiment of the invention, each rib has a width of between 0.3 mm and 1.6 mm, preferably between 0.4 mm and 1.5 mm, each rib has a height of between 0.8. mm and 2.7 mm, preferably between 1.0 mm and 2.5 mm, and the plate has a thickness of between 0.6 mm and 1.7 mm, preferably between 0.8 mm and 1.5 mm .

Ainsi, une telle largeur de nervure confère à chaque nervure une résistance mécanique élevée, ce qui permet notamment de diminuer le risque d'inflammation de l'aluminium, lorsqu'un fluide est de l'oxygène, car l'élément d'échangeur monobloc peut être fabriqué avec une largeur de nervure plus grande que dans l'art antérieur.Thus, such a rib width gives each rib a high mechanical strength, which in particular reduces the risk of ignition of aluminum, when a fluid is oxygen because the monobloc exchanger element can be manufactured with a larger rib width than in the prior art.

Ainsi, une telle largeur de nervure confère à la plaque une résistance mécanique élevée, ce qui permet notamment de diminuer le risque d'inflammation de l'aluminium, lorsqu'un fluide est de l'oxygène, car l'élément d'échangeur monobloc peut être fabriqué avec une plaque plus épaisse que dans l'art antérieurThus, such a rib width gives the plate a high mechanical strength, which in particular reduces the risk of ignition of aluminum, when a fluid is oxygen, because the monobloc exchanger element can be made with a thicker plate than in the prior art

Selon une variante de l'invention, des nervures présentent des encoches agencées de manière à permettre une communication entre des canaux consécutifs. Ainsi, de telles encoches permettent l'écoulement de fluide calorigène ou de fluide frigorigène entre deux canaux consécutifs.According to a variant of the invention, ribs have notches arranged so as to allow communication between consecutive channels. Thus, such notches allow the flow of circulating fluid or refrigerant between two consecutive channels.

Selon une variante de l'invention, les nervures sont agencées de sorte que chaque canal a une largeur comprise entre 0,8 mm et 1,2 mm. Ainsi, des tels canaux permettent d'assurer des débits élevés de fluide calorigène et de fluide frigorigène.According to a variant of the invention, the ribs are arranged so that each channel has a width of between 0.8 mm and 1.2 mm. Thus, such channels can ensure high flows of circulating fluid and refrigerant.

Selon un mode de réalisation de l'invention, le matériau formant la plaque, les nervures et les barres de fermeture monoblocs est sélectionné dans le groupe constitué par du cuivre, des alliages de cuivre, d'un acier inoxydable, de l'aluminium, les alliages d'aluminium en particulier de nuance 3003, 3004, 3104 et 3005, les alliages de brasage plaqués 4004, 4104, 4343, 4045, 4047A et leur association avec ceux de la famille 3000According to one embodiment of the invention, the material forming the plate, the ribs and the one-piece closure bars is selected from the group consisting of copper, copper alloys, a stainless steel, aluminum, aluminum alloys in particular of grade 3003, 3004, 3104 and 3005, plated brazing alloys 4004, 4104, 4343, 4045, 4047A and their combination with those of the 3000 family

Ainsi, un tel matériau permet de réaliser un élément d'échange mécaniquement résistant.Thus, such a material makes it possible to produce a mechanically resistant exchange element.

Selon une variante de l'invention, l'élément d'échangeur comprend de la brasure disposée sur des nervures et/ou sur au moins une barre de fermeture. De manière alternative ou complémentaire, l'élément d'échangeur comprend de la brasure disposée sur une face de la plaque dépourvue de nervures, le cas échéant. Ainsi, une telle brasure permet de solidariser les éléments d'échangeur deux à deux.According to a variant of the invention, the exchanger element comprises solder disposed on ribs and / or on at least one closure bar. Alternatively or additionally, the exchanger element comprises solder disposed on a face of the plate without ribs, if any. Thus, such a solder makes it possible to secure the exchanger elements in pairs.

Selon un mode de réalisation de l'invention, des nervures s'étendent, en saillie sur au moins une face de la plaque, parallèlement entre elles de façon à former des parois de canaux dits d'échange parallèles entre eux.According to one embodiment of the invention, ribs extend, projecting on at least one face of the plate, parallel to each other so as to form so-called exchange channel walls parallel to each other.

Ainsi, de tels canaux d'échange parallèles permettent de faire circuler du fluide calorigène ou du fluide frigorigène avec relativement peu de pertes de charge et sur la majeure partie de la longueur de la plaque.Thus, such parallel exchange channels can circulate the circulating fluid or refrigerant with relatively low pressure losses and over most of the length of the plate.

Selon une forme de réalisation du mode de réalisation précédent, les canaux de distribution s'étendent suivant des angles compris entre 45° et 90° par rapport aux canaux d'échange.According to one embodiment of the preceding embodiment, the distribution channels extend at angles between 45 ° and 90 ° with respect to the exchange channels.

Ainsi, un tel agencement des nervures permet de privilégier la distribution de fluide calorigène et de fluide frigorigène, car la perte de charge générée dans la région des canaux d'échange est supérieure à la perte de charge générée dans chaque région des canaux de distribution.Thus, such an arrangement of the ribs makes it possible to favor the distribution of circulating fluid and refrigerant, since the pressure drop generated in the region of the exchange channels is greater than the pressure drop generated in each region of the distribution channels.

Selon une variante du mode de réalisation précédent, le diamètre hydraulique des canaux de distribution est supérieur au diamètre hydraulique des canaux d'échange. Ainsi, de tels diamètres hydrauliques permettent de faciliter la distribution de fluide calorigène et de fluide frigorigène, car la perte de charge générée dans la région des canaux d'échange est supérieure à la perte de charge générée dans chaque région des canaux de distribution. Les diamètres hydrauliques peuvent être variables au gré des canaux d'échange alimentés (cas des canaux usinés chimiquement).According to a variant of the previous embodiment, the hydraulic diameter of the distribution channels is greater than the hydraulic diameter of the exchange channels. Thus, such hydraulic diameters facilitate the distribution of circulating fluid and refrigerant, because the pressure drop generated in the region of the exchange channels is greater than the pressure drop generated in each region of the distribution channels. The hydraulic diameters can be variable according to the exchange channels supplied (chemically machined channels).

Selon une forme de réalisation des deux modes de réalisation précédents :

  • la première face de la plaque comporte des nervures formant des parois de canaux d'échange parallèles ; et
  • la deuxième face de la plaque comporte i) des nervures formant des parois de canaux d'échange ainsi que ii) des nervures formant des parois de canaux de distribution transversaux aux canaux d'échange.
According to one embodiment of the two previous embodiments:
  • the first face of the plate has ribs forming walls of parallel exchange channels; and
  • the second face of the plate comprises i) ribs forming walls of exchange channels and ii) ribs forming distribution channel walls transverse to the exchange channels.

Ainsi, un tel élément d'échangeur « hybride » a une face qui remplit uniquement la fonction d'échange de chaleur, tandis que l'autre face remplit aussi une fonction de distribution de fluides.Thus, such a "hybrid" heat exchanger element has one side that only fulfills the heat exchange function, while the other side also performs a fluid distribution function.

Par ailleurs, la présente invention a pour objet un échangeur de chaleur, pour une unité de séparation de gaz par cryogénie, comprenant plusieurs éléments d'échangeur empilés et solidarisés entre eux, par exemple au moyen de brasure, de sorte que les plaques s'étendent parallèlement entre elles, l'échangeur de chaleur étant caractérisé en ce qu'il comprend plusieurs éléments d'échangeur selon l'invention, de préférence tous les éléments d'échangeur sont selon l'invention.Furthermore, the subject of the present invention is a heat exchanger, for a cryogenic gas separation unit, comprising several exchanger elements stacked and joined together, for example by means of solder, so that the plates extend parallel to each other, the heat exchanger being characterized in that it comprises several exchanger elements according to the invention, preferably all the exchanger elements are according to the invention.

Ainsi, un tel échangeur de chaleur présente une résistance mécanique très élevée, ce qui lui permet de fonctionner sous des pressions de fluide calorigène et/ou frigorigène supérieures à 50 bar A, voire à 80 bar A, voire même à 100 bar A.Thus, such a heat exchanger has a very high mechanical strength, which allows it to operate under fluid pressures calorigenic and / or refrigerant greater than 50 bar A, or even 80 bar A, or even 100 bar A.

Selon une forme de réalisation du mode de réalisation précédent, des éléments d'échangeur précités à canaux d'échange sont empilés en alternance avec des éléments d'échangeur précités à canaux de distribution et canaux d'échange.According to one embodiment of the preceding embodiment, exchange-channel exchanger elements mentioned above are stacked alternately with the above-mentioned exchanger elements with distribution channels and exchange channels.

En d'autres termes, cet échangeur de chaleur comprend un empilement d'éléments d'échangeur dont au moins un sur deux a des canaux de distribution.In other words, this heat exchanger comprises a stack of exchanger elements of which at least one in two has distribution channels.

Ainsi, de tels canaux de distribution permettent de distribuer le fluide calorigène ou le fluide frigorigène vers les canaux d'échange où se produit essentiellement l'échange de chaleur.Thus, such distribution channels make it possible to distribute the heat transfer fluid or the refrigerant towards the exchange channels in which the heat exchange essentially occurs.

Par ailleurs, la présente invention a pour objet un procédé de fabrication, pour fabriquer un élément d'échangeur pour un échangeur de chaleur destiné à transférer de la chaleur d'au moins un fluide primaire dit fluide calorigène vers au moins un fluide secondaire dit fluide frigorigène, le procédé de fabrication comprenant les étapes :

  • une première étape éventuelle d'usinage chimique de certaines zones des plaques (ex distribution) ;
  • presser et déplacer un outil contre au moins une face de l'ébauche de plaque avec une pression permettant de déformer plastiquement l'ébauche de plaque, de façon à former des premières nervures, formant des parois de canaux d'échange, qui s'étendent en saillie sur au moins une première face d'une plaque issue de l'ébauche de plaque ;
  • presser et déplacer l'outil contre ladite au moins une première face de l'ébauche de plaque, de façon à former des nervures formant des parois des canaux de distribution et
  • déformer plastiquement l'ébauche de plaque, de façon à former des barres de fermeture s'étendant suivant des bords de la plaque issue de l'ébauche de plaque.
Moreover, the subject of the present invention is a manufacturing method, for manufacturing an exchanger element for a heat exchanger intended to transfer heat from at least one primary fluid known as caloric fluid to at least one secondary fluid called fluid. refrigerant, the manufacturing process comprising the steps of:
  • a first possible step of chemical machining of certain areas of the plates (ex distribution);
  • pressing and moving a tool against at least one face of the plate blank with a pressure to plastically deform the plate blank, so as to form first ribs, forming exchange channel walls, which extend protruding on at least a first face of a plate from the plate blank;
  • pressing and moving the tool against said at least one first face of the plate blank, so as to form ribs forming walls of the distribution channels and
  • plastically deforming the plate blank, so as to form closure bars extending along edges of the plate from the blank plate.

Ainsi, un tel procédé de fabrication permet de fabriquer, à partir d'une ébauche de plaque et de manière rapide, un élément d'échangeur selon l'invention qui a une résistance mécanique très élevée et qui a des canaux d'échange et des canaux de distribution.Thus, such a manufacturing method makes it possible to manufacture, from a plate blank and in a fast manner, an exchanger element according to the invention has a very high mechanical strength and has exchange channels and distribution channels.

Selon une variante de l'invention, l'ébauche de plaque a une épaisseur supérieure à 1 mm. Ainsi, une telle épaisseur permet de fabriquer une plaque ayant une résistance mécanique très élevée, car la plaque est relativement épaisse.According to a variant of the invention, the plate blank has a thickness greater than 1 mm. Thus, such a thickness makes it possible to manufacture a plate having a very high mechanical strength, because the plate is relatively thick.

Selon un mode de réalisation de l'invention, l'outil comprend au moins deux roulettes coaxiales et séparées d'une distance correspondant à une largeur d'une nervure, les roulettes se déplaçant par roulement contre ladite au moins une face de l'ébauche de plaque.According to one embodiment of the invention, the tool comprises at least two coaxial wheels and separated by a distance corresponding to a width of a rib, the rollers rolling against said at least one face of the blank plate.

Ainsi, de telles roulettes permettent de réaliser des nervures de manière précise et rapide.Thus, such wheels make it possible to make ribs accurately and quickly.

Les modes de réalisation de l'invention et les variantes de l'invention mentionnés ci-avant peuvent être pris isolément ou selon toute combinaison techniquement possible.The embodiments of the invention and the variants of the invention mentioned above can be taken individually or in any combination technically possible.

La présente invention sera bien comprise et ses avantages ressortiront aussi à la lumière de la description qui va suivre, donnée uniquement à titre d'exemple non limitatif et faite en référence aux dessins annexés, dans lesquels :

  • la figure 1 est une vue en perspective, avec transparence, d'une partie d'un élément d'échangeur selon l'art antérieur ;
  • la figure 2 est une vue de dessus de l'élément d'échangeur de la figure 1 ;
  • la figure 3 est une vue similaire à la figure 2 d'un élément d'échangeur conforme à l'invention ;
  • la figure 4 est une vue de dessus, avec troncature, d'un élément d'échangeur conforme à l'invention ; et
  • la figure 5 est une vue en section d'une partie d'un échangeur de chaleur comprenant un élément d'échangeur qui ne fait pas partie de l'invention.
The present invention will be well understood and its advantages will also emerge in the light of the description which follows, given solely by way of nonlimiting example and with reference to the appended drawings, in which:
  • the figure 1 is a perspective view, with transparency, of a part of an exchanger element according to the prior art;
  • the figure 2 is a top view of the exchanger element of the figure 1 ;
  • the figure 3 is a view similar to the figure 2 an exchanger element according to the invention;
  • the figure 4 is a top view, with truncation, of an exchanger element according to the invention; and
  • the figure 5 is a sectional view of a portion of a heat exchanger comprising an exchanger element which does not form part of the invention.

La figure 1 illustre une partie d'un élément d'échangeur 1 adapté pour composer un échangeur de chaleur destiné à transférer de la chaleur d'au moins un fluide primaire dit fluide calorigène vers au moins un fluide secondaire dit fluide frigorigène.The figure 1 illustrates a part of an exchanger element 1 adapted to compose a heat exchanger for transferring heat from at least one primary fluid called caloric fluid to at least one secondary fluid called refrigerant.

Comme le montrent les figures 1 et 2, l'élément d'échangeur 1 comporte une plaque 2, des nervures 4 et des barres de fermeture 8.1 et 8.3. La plaque 2, les nervures 4 et les barres de fermeture 8.1 et 8.3 sont monoblocs. Dans l'exemple des figures 1 et 2, la plaque 2, toutes les nervures 4 et toutes les barres de fermeture 8.1 et 8.3 sont monoblocs. Usuellement, les nervures sont aussi dénommées « ailettes ». Usuellement, la plaque est aussi dénommée « base ».As shown by Figures 1 and 2 , the exchanger element 1 comprises a plate 2, ribs 4 and closing bars 8.1 and 8.3. The plate 2, the ribs 4 and the closing bars 8.1 and 8.3 are monobloc. In the example of Figures 1 and 2 , the plate 2, all the ribs 4 and all the closing bars 8.1 and 8.3 are monobloc. Usually, the ribs are also called "fins". Usually, the plate is also called "base".

En d'autres termes, la plaque 2, les nervures 4 et les barres de fermeture 8.1 et 8.3 sont réalisées en une seule pièce, donc composées d'un seul et même matériau. Dans l'exemple des figures 1 et 2, le matériau formant l'ensemble monobloc composé de la plaque 2, les nervures 4 et les barres de fermeture 8.1 et 8.3 est ici un alliage d'aluminium de nuance 3003.In other words, the plate 2, the ribs 4 and the closing bars 8.1 and 8.3 are made in one piece, and therefore composed of a single material. In the example of Figures 1 and 2 , the material forming the one-piece assembly composed of the plate 2, the ribs 4 and the closing bars 8.1 and 8.3 is here an aluminum alloy of grade 3003.

La plaque 2 est pleine, plate et elle a globalement la forme d'un rectangle. Les bords de la plaque 2 s'étendent respectivement suivant une direction longitudinale X2 et une direction latérale Y2.The plate 2 is full, flat and generally has the shape of a rectangle. The edges of the plate 2 extend respectively in a longitudinal direction X2 and a lateral direction Y2.

Les nervures 4 s'étendent ici en saillie sur une seule face de la plaque 2. La face opposée 2.1 est dépourvue de nervures. Chaque nervure 4 forme une portion d'une paroi d'un canal respectif 6. Les nervures ont ici des sections transversales, dans un plan perpendiculaire à la direction longitudinale X2, qui sont rectangulaires et semblables entre elles.The ribs 4 extend here projecting on one side of the plate 2. The opposite face 2.1 is devoid of ribs. Each rib 4 forms a portion of a wall of a respective channel 6. The ribs here have cross sections, in a plane perpendicular to the longitudinal direction X2, which are rectangular and similar to each other.

Chaque canal 6 est adapté pour l'écoulement de fluide calorigène ou de fluide frigorigène. Comme les nervures 4 s'étendent parallèlement entre elles et à la direction longitudinale X2, les canaux 6 sont parallèles entre eux et à la direction longitudinale X2.Each channel 6 is adapted for the flow of circulating fluid or refrigerant. As the ribs 4 extend parallel to each other and to the longitudinal direction X2, the channels 6 are parallel to each other and to the longitudinal direction X2.

Chaque canal 6 est délimité par une nervure 4 de l'élément d'échangeur 1, par une nervure de l'élément d'échangeur adjacent et par la plaque 2, laquelle définit le « fond » du canal 6.Each channel 6 is delimited by a rib 4 of the exchanger element 1, by a rib of the adjacent exchanger element and by the plate 2, which defines the "bottom" of the channel 6.

En service, chaque canal 6 canalise du fluide calorigène ou du fluide frigorigène, selon qu'il est alimenté en fluide calorigène ou en fluide frigorigène. Les canaux 6 sont dits canaux d'échange, car ils contribuent à remplir la fonction de transfert de chaleur entre du fluide calorigène et du fluide frigorigène par l'intermédiaire notamment de la plaque 2.In use, each channel 6 channels the circulating fluid or refrigerant, depending on whether it is supplied with circulating fluid or refrigerant. The channels 6 are called exchange channels, since they contribute to fulfilling the function of heat transfer between the circulating fluid and the refrigerant via, in particular, the plate 2.

Comme le montre la figure 2, l'élément d'échangeur 1 comporte deux barres de fermeture 8.1 et 8.3. Les barres de fermeture 8.1 et 8.3 s'étendent respectivement le long de deux bords de la plaque 2. Les barres de fermeture 8.1 et 8.3 s'étendent parallèlement à la direction longitudinale X2.As shown in figure 2 , the exchanger element 1 comprises two closing bars 8.1 and 8.3. The closing bars 8.1 and 8.3 extend respectively along two edges of the plate 2. The closing bars 8.1 and 8.3 extend parallel to the longitudinal direction X2.

Les barres de fermeture 8.1 et 8.3 s'étendent suivant des bords de la plaque 2 de façon à obturer des canaux 6. Les barres de fermeture 8.1, et 8.3 bordent, donc obturent respectivement un canal 6 situé près d'un bord latéral de la plaque 2.The closure bars 8.1 and 8.3 extend along the edges of the plate 2 so as to close the channels 6. The closing bars 8.1, and 8.3 line, thus close respectively a channel 6 located near a lateral edge of the plate 2.

Les barres de fermeture 8.1 et 8.3 sont ici agencées de sorte que tous les bords de la plaque 2 sont longés par une barre de fermeture respective 8.1 et 8.3. Alternativement, chaque bord de la plaque 2 peut être longé par plusieurs barres de fermeture distinctes. Alternativement encore, en tant que de besoin, au moins un bord de la plaque peut présenter un tronçon de sa longueur qui n'est pas longé par une barre de fermeture.The closing bars 8.1 and 8.3 are here arranged so that all the edges of the plate 2 are bordered by a respective closing bar 8.1 and 8.3. Alternatively, each edge of the plate 2 may be bordered by several separate closing bars. Alternatively again, as needed, at least one edge of the plate may have a portion of its length which is not bordered by a closing bar.

De plus, de manière connue en soi mais non représentée, chaque barre de fermeture peut comporter une ouverture, usuellement dénommée « fenêtre », pour introduire ou évacuer du fluide respectivement dans ou hors des canaux.In addition, in a manner known per se but not shown, each closure bar may comprise an opening, usually called "window", for introducing or discharging fluid respectively into or out of the channels.

Dans l'exemple des figures 1 et 2, la plaque 2 a une épaisseur E2 d'environ 1,2 mm. Chaque nervure 4 a une largeur W4 d'environ 0,5 mm et une hauteur H4 d'environ 1,8 mm. Chaque canal 6 a une largeur W6 d'environ 1,0 mm.In the example of Figures 1 and 2 the plate 2 has a thickness E2 of about 1.2 mm. Each rib 4 has a width W4 of about 0.5 mm and a height H4 of about 1.8 mm. Each channel 6 has a width W6 of about 1.0 mm.

La plaque 2 a une longueur L2 d'environ 6 m, mesurée suivant la direction longitudinale X2. La plaque 2 a une largeur W2 d'environ 2,5 m, mesurée suivant la direction transversale Y2.The plate 2 has a length L2 of about 6 m measured in the longitudinal direction X2. The plate 2 has a width W2 of about 2.5 m, measured in the transverse direction Y2.

L'élément d'échangeur 1 comprend de la brasure disposée sur les nervures 4 et sur les barres de fermeture 8.1 et 8.3. Cette brasure forme une couche d'environ 0,1 mm d'épaisseur. En complément, l'élément d'échangeur 1 comprend de la brasure disposée sur la face 2.1 de la plaque 2, c'est-à-dire la face dépourvue de nervures. Ces couches de brasure permettent de solidariser entre eux plusieurs éléments d'échangeurs empilés et chauffés dans un four à vide, de manière connue en soi.The exchanger element 1 comprises solder disposed on the ribs 4 and on the closing bars 8.1 and 8.3. This solder forms a layer about 0.1 mm thick. In addition, the exchanger element 1 comprises solder disposed on the face 2.1 of the plate 2, that is to say the face without ribs. These solder layers make it possible to join together several exchanger elements stacked and heated in a vacuum oven, in a manner known per se.

La figure 3 illustre un élément d'échangeur 101 conforme à l'invention. Dans la mesure où l'élément d'échangeur 101 est similaire à l'élément d'échangeur 1, la description de l'élément d'échangeur 1 donnée ci-avant en relation avec les figures 1 et 2 peut être transposée à l'élément d'échangeur 101, à l'exception des différences notables énoncées ci-après.The figure 3 illustrates an exchanger element 101 according to the invention. Insofar as the exchanger element 101 is similar to the exchanger element 1, the description of the exchanger element 1 given above in relation to the Figures 1 and 2 can be transposed to the exchanger element 101, with the exception of the notable differences set out below.

Un composant de l'élément d'échangeur 101 identique ou correspondant, par sa structure ou par sa fonction, à un composant de l'élément d'échangeur 1 porte la même référence numérique augmentée de 100. On définit ainsi une plaque 102, des nervures 104 définissant des canaux d'échange 106, ainsi que des barres de fermeture 108.1, 108.2, 108.3 et 108.4.A component of the exchanger element 101 which is identical or corresponding, in structure or function, to a component of the exchanger element 1 has the same numerical reference increased by 100. Thus, a plate 102 is defined. ribs 104 defining exchange channels 106, as well as closing bars 108.1, 108.2, 108.3 and 108.4.

L'élément d'échangeur 101 diffère de l'élément d'échangeur 1, notamment car l'élément d'échangeur 101 a des nervures 105 qui sont agencées, en saillie sur une face de la plaque 102, de façon à former des parois de deuxièmes canaux dits canaux de distribution 107, de sorte que les canaux de distribution 107 s'étendent transversalement aux canaux d'échange 106. Comme le montre la figure 3, les canaux de distribution 107 s'étendent suivant des angles d'environ 90° par rapport aux canaux d'échange 106.The exchanger element 101 differs from the exchanger element 1, in particular since the exchanger element 101 has ribs 105 which are arranged, projecting on one face of the plate 102, so as to form walls. second channels said distribution channels 107, so that the distribution channels 107 extend transversely to the exchange channels 106. As shown in FIG. figure 3 the distribution channels 107 extend at angles of about 90 ° to the exchange channels 106.

L'agencement des nervures 105 permet de privilégier la distribution de fluide calorigène ou de fluide frigorigène, car la perte de charge générée dans la région des canaux d'échange 106 est supérieure à la perte de charge générée dans chaque région des canaux de distribution 107.The arrangement of the ribs 105 makes it possible to favor the distribution of circulating fluid or refrigerant, since the pressure drop generated in the region of the exchange channels 106 is greater than the pressure drop generated in each region of the distribution channels. .

De plus, l'élément d'échangeur 101 diffère de l'élément d'échangeur 1, car l'élément d'échangeur 101 comporte quatre barres de fermeture 108.1, 108.2, 108.3, 108.4 qui s'étendent respectivement le long des quatre bords de la plaque 102. Les barres de fermeture 108.1, 108.2, 108.3, 108.4 sont parallèles deux à deux.In addition, the exchanger element 101 differs from the exchanger element 1, because the exchanger element 101 has four closing bars 108.1, 108.2, 108.3, 108.4 which extend respectively along the four edges. of the plate 102. The closing bars 108.1, 108.2, 108.3, 108.4 are parallel in pairs.

La figure 4 illustre un élément d'échangeur 201 conforme à l'invention. Dans la mesure où l'élément d'échangeur 201 est similaire à l'élément d'échangeur 101, la description de l'élément d'échangeur 101 donnée ci-avant en relation avec la figure 3 peut être transposée à l'élément d'échangeur 201, à l'exception des différences notables énoncées ci-après.The figure 4 illustrates an exchanger element 201 according to the invention. Insofar as the exchanger element 201 is similar to the exchanger element 101, the description of the exchanger element 101 given above in relation to the figure 3 may be transposed to the exchanger element 201, with the exception of the notable differences set out below.

Un composant de l'élément d'échangeur 201 identique ou correspondant, par sa structure ou par sa fonction, à un composant de l'élément d'échangeur 101 porte la même référence numérique augmentée de 100. On définit ainsi une plaque 202, des nervures 204 définissant des canaux d'échange 206, ainsi que des barres de fermeture 208.1, 208.3 et 208.4 et équivalent, représentées en tirets.A component of the exchanger element 201 which is identical or corresponding, in structure or function, to a component of the exchanger element 101 has the same numerical reference increased by 100. Thus, a plate 202, ribs 204 defining exchange channels 206, as well as closing bars 208.1, 208.3 and 208.4 and the like, shown in dashed lines.

L'élément d'échangeur 201 diffère de l'élément d'échangeur 101, notamment car l'élément d'échangeur 201 a des nervures 205 qui sont agencées, en saillie sur une face de la plaque 202, de façon à former des parois de canaux de distribution 207, de sorte que les canaux de distribution 207 s'étendent obliquement aux canaux d'échange 206. Comme le montre la figure 4, les canaux de distribution 207 s'étendent suivant des angles d'environ 45° par rapport aux canaux d'échange 206.The exchanger element 201 differs from the exchanger element 101, in particular because the exchanger element 201 has ribs 205 which are arranged, projecting on one face of the plate 202, so as to form walls distribution channels 207, so that the distribution channels 207 extend obliquely to the exchange channels 206. As shown in FIG. figure 4 , the distribution channels 207 extend at angles of approximately 45 ° with respect to the exchange channels 206.

L'agencement des nervures 205 permet de privilégier davantage la distribution de fluide calorigène ou de fluide frigorigène, car la perte de charge générée dans la région des canaux d'échange 206 est supérieure à la perte de charge générée dans chaque région des canaux de distribution 207.The arrangement of the ribs 205 makes it possible to give greater priority to the distribution of circulating fluid or refrigerant, since the pressure drop generated in the region of the exchange channels 206 is greater than the pressure drop generated in each region of the distribution channels. 207.

Pour alimenter l'élément d'échangeur 201 ou l'élément d'échangeur 101, un échangeur de chaleur conforme à l'invention comprend en outre des boîtes d'alimentation non représentées qui sont solidarisées, par exemple par soudure, sur des faces externes respectives de l'échangeur de chaleur.To feed the exchanger element 201 or the exchanger element 101, a heat exchanger according to the invention also comprises unrepresented feed boxes which are secured, for example by welding, on external faces. of the heat exchanger.

Ainsi, de telles boîtes d'alimentation permettent l'entrée ou la sortie de fluide calorigène ou de fluide frigorigène dans ou hors des canaux de distribution 107 ou 207, donc dans ou hors des canaux d'échange 106 ou 206.Thus, such feed boxes allow the entry or exit of circulating fluid or refrigerant in or out of the distribution channels 107 or 207, so in or out of the exchange channels 106 or 206.

Dans l'exemple des figures 3 et 4, les boîtes d'alimentation peuvent être disposées sur les portions d'extrémités longitudinales de l'élément d'échangeur 101 ou 201, de sorte que ces boîtes d'alimentation sont raccordées fluidiquement aux passages définis par l'ensemble des canaux de distribution 107 ou 207.In the example of figures 3 and 4 , the feed boxes can be arranged on the longitudinal end portions of the exchanger element 101 or 201, so that these feed boxes are fluidly connected to the passages defined by all of the distribution channels 107 or 207.

La figure 5 illustre un échangeur de chaleur 300 pour composer une unité non représentée de séparation de gaz par cryogénie. L'échangeur de chaleur 300 comprend plusieurs éléments d'échangeur 301, 321, 341 etc. conformes à l'invention, qui sont empilés et solidarisés entre eux au moyen de brasure.The figure 5 illustrates a heat exchanger 300 for composing a unit not shown cryogenic gas separation. The heat exchanger 300 comprises several exchanger elements 301, 321, 341 and so on. according to the invention, which are stacked and joined together by means of solder.

Dans la mesure où l'élément d'échangeur 301, 321 ou 341 est similaire à l'élément d'échangeur 1 ou 101, la description de l'élément d'échangeur 1 ou 101 donnée ci-avant en relation avec les figures 1, 2 ou 3 peut être transposée à l'élément d'échangeur 301, 321 ou 341, à l'exception des différences notables énoncées ci-après.Insofar as the exchanger element 301, 321 or 341 is similar to the exchanger element 1 or 101, the description of the exchanger element 1 or 101 given above in relation to the Figures 1, 2 or 3 may be transposed to the exchanger element 301, 321 or 341, with the exception of the notable differences set forth below.

Un composant de l'élément d'échangeur 301, 321 ou 341 identique ou correspondant, par sa structure ou par sa fonction, à un composant de l'élément d'échangeur 1 ou 101 porte la même référence numérique augmentée de 100 ou 200. On définit ainsi des plaques 302, 322, 342, des canaux d'échange 306, 326, 346 et des barres de fermeture 308, 328, 348.A component of the exchanger element 301, 321 or 341 identical or corresponding, by its structure or function, to a component of the exchanger element 1 or 101 has the same numerical reference increased by 100 or 200. Thus plates 302, 322, 342, exchange channels 306, 326, 346 and closing bars 308, 328, 348 are defined.

La figure 5 illustre une section transversale dans un plan perpendiculaire à la direction longitudinale et passant par la région médiane des éléments d'échangeur 301, 321 ou 341, c'est-à-dire une région présentant seulement des canaux d'échange 306, 326 et 346. Les plaques 302, 322, 342 s'étendent parallèlement entre elles.The figure 5 illustrates a cross-section in a plane perpendicular to the longitudinal direction and passing through the middle region of the exchanger elements 301, 321 or 341, i.e. a region having only exchange channels 306, 326 and 346 The plates 302, 322, 342 extend parallel to one another.

L'élément d'échangeur 301, 321 ou 341 diffère de l'élément d'échangeur 101, notamment car l'élément d'échangeur 301, 321 ou 341 a des nervures qui s'étendent en saillie sur les deux faces de la plaque respective 302, 322 ou 342.The heat exchanger element 301, 321 or 341 differs from the heat exchanger element 101, in particular because the heat exchanger element 301, 321 or 341 has ribs which protrude on both sides of the plate. respective 302, 322 or 342.

Ainsi, l'élément d'échangeur 301 a des nervures 304.1 sur une première face et des nervures 304.2 sur sa deuxième face. De même, l'élément d'échangeur 321 a des nervures 324.1 sur une première face et des nervures 324.2 sur sa deuxième face, et l'élément d'échangeur 341 a des nervures 344.1 sur une première face et des nervures 344.2 sur sa deuxième face.Thus, the exchanger element 301 has ribs 304.1 on a first face and ribs 304.2 on its second face. Likewise, the exchanger element 321 has ribs 324.1 on a first face and ribs 324.2 on its second face, and the exchanger element 341 has ribs 344.1 on one face and ribs 344.2 on its second face. face.

De plus, l'élément d'échangeur 301, 321 ou 341 diffère de l'élément d'échangeur 101, car la première face de la plaque 302, 322 ou 342 comporte des nervures formant des parois de canaux d'échange 306 parallèles. Tandis que la deuxième face de la plaque 302, 322 ou 342 comporte, d'une part, des nervures 304.2, 324.1 formant des parois de canaux d'échange 326 ainsi que, d'autre part, des nervures non représentées formant des parois de canaux de distribution qui sont transversaux par rapport aux canaux d'échange 326 comme les canaux de distribution 207.In addition, the exchanger element 301, 321 or 341 differs from the exchanger element 101, since the first face of the plate 302, 322 or 342 has ribs forming walls of parallel exchange channels 306. While the second face of the plate 302, 322 or 342 comprises, on the one hand, ribs 304.2, 324.1 forming walls of exchange channels 326 and, on the other hand, ribs not shown forming walls of distribution channels that are transverse to exchange channels 326 such as distribution channels 207.

En d'autres termes, l'échangeur de chaleur 300 comprend un empilement d'éléments d'échangeur 301, 321, 341 dont un sur deux a des canaux de distribution semblables aux canaux de distribution 207.In other words, the heat exchanger 300 comprises a stack of heat exchanger elements 301, 321, 341 of which one in two has distribution channels similar to the distribution channels 207.

En d'autres termes, l'élément d'échangeur 301, 321 ou 341 est « hybride », car il présente seulement des canaux d'échange sur une face, et des canaux d'échange plus des canaux de distribution sur la face opposée.In other words, the exchanger element 301, 321 or 341 is "hybrid" because it only has exchange channels on one side, and exchange channels plus distribution channels on the opposite side .

Alternativement à cet empilement d'éléments d'échangeur hybrides, l'échangeur de chaleur peut comprendre des éléments d'échangeur avec canaux d'échange qui sont empilés en alternance avec des éléments d'échangeur avec canaux de distribution.Alternatively to this stack of hybrid exchanger elements, the heat exchanger may comprise exchanger elements with exchange channels which are stacked alternately with exchanger elements with distribution channels.

Dans l'exemple de la figure 5, les nervures 304.1, 324.1 ou 344.1 de la première face sont décalées par rapport aux nervures respectives 304.2, 324.2 ou 344.2 de la deuxième face. En d'autres termes, les nervures 304.1, 324.1 ou 344.1 de la première face ne sont pas situées au droit des nervures respectives 304.2, 324.2 ou 344.2 de la deuxième face.In the example of the figure 5 , the ribs 304.1, 324.1 or 344.1 of the first face are offset with respect to the respective ribs 304.2, 324.2 or 344.2 of the second face. In other words, the ribs 304.1, 324.1 or 344.1 of the first face are not located in line with the respective ribs 304.2, 324.2 or 344.2 of the second face.

Sur une première face de la plaque 302, deux nervures consécutives 304.1 sont distantes d'un premier pas P304.1, et sur une deuxième face de la plaque 302, deux nervures consécutives 304.2 sont distantes d'un deuxième pas P304.2 qui est supérieur au premier pas P304.1.On a first face of the plate 302, two consecutive ribs 304.1 are spaced apart by a first pitch P304.1, and on a second face of the plate 302, two consecutive ribs 304.2 are spaced apart by a second pitch P304.2 which is greater than the first step P304.1.

Dans l'exemple de la figure 5, le deuxième pas P304.2 vaut 1,5 fois le premier pas. Ainsi, les canaux 306 et 326, après empilement des éléments d'échangeur 301 et 321, ont des largeurs différentes.In the example of the figure 5 , the second step P304.2 is 1.5 times the first step. Thus, the channels 306 and 326, after stacking of the exchanger elements 301 and 321, have different widths.

De plus, sur chaque face de la plaque 302, la nervure latérale 304.1 qui est la nervure la plus proche du bord gauche de la plaque 301 est distante de la barre de fermeture correspondante 308 d'environ 1 fois le pas P304.1. La nervure latérale opposée non représentée, qui est la nervure la plus proche du bord opposé de la plaque 302, est distante de la barre de fermeture correspondante non représentée d'environ 2 fois le pas.In addition, on each face of the plate 302, the lateral rib 304.1 which is the rib closest to the left edge of the plate 301 is spaced from the corresponding closing bar 308 by approximately 1 times the pitch P304.1. The opposite lateral rib, not shown, which is the rib closest to the opposite edge of the plate 302, is spaced from the corresponding not shown closing bar by approximately twice the pitch.

Ainsi, on peut alterner un élément d'échangeur 301 tourné vers le haut avec un élément d'échangeur identique, tel 321, tourné vers le bas, ce qui permet de former des canaux 306 et 326 de largeurs différentes entre les deux faces de la plaque 302.Thus, it is possible to alternate an exchanger element 301 facing upwards with an identical exchanger element, such as 321, facing downwards, which makes it possible to form channels 306 and 326 of different widths between the two faces of the plate 302.

Pour fabriquer l'élément d'échangeur 1, le procédé de fabrication comprend les étapes :

  • apposer un masque ;
  • plonger les plaques dans les bains d'usinage chimique ;
  • presser et déplacer un outil non représenté contre une face de l'ébauche de plaque avec une pression permettant de déformer plastiquement l'ébauche de plaque, de façon à former les nervures 4 en saillie sur une face de la plaque 2 issue de l'ébauche de plaque ; et
  • déformer plastiquement l'ébauche de plaque, de façon à former les barres de fermeture 8 s'étendant suivant les bords de la plaque 2 issue de l'ébauche de plaque.
To manufacture the exchanger element 1, the manufacturing process comprises the steps of:
  • affix a mask;
  • plunge the plates into the chemical machining baths;
  • pressing and moving a tool not shown against a face of the blank plate with a pressure for plastically deforming the blank plate, so as to form the ribs 4 projecting on a face of the plate 2 from the blank plate; and
  • plastically deforming the blank plate, so as to form the closure bars 8 extending along the edges of the plate 2 from the blank plate.

L'étape de déformation plastique de l'ébauche de plaque est effectuée par déplacement de la matière, mais sans enlèvement de matière.The step of plastic deformation of the plate blank is performed by moving the material, but without removing material.

Selon une étape de ce procédé de fabrication, l'ébauche de plaque a une épaisseur d'environ 2 mm.According to a step of this manufacturing method, the plate blank has a thickness of about 2 mm.

Suivant le procédé de fabrication de l'élément selon l'invention, on prévoit plusieurs passages avec des outils différents, de façon à réaliser des nervures par étapes successives. Cela permet de déformer l'ébauche de plaque de manière progressive, ce qui évite les risques de rupture et ce qui limite les efforts à produire et les contraintes sur les outils.According to the manufacturing method of the element according to the invention, several passages are provided with different tools, so as to make ribs in successive steps. This makes it possible to deform the plate blank in a progressive manner, which avoids the risks of rupture and which limits the efforts to be made and the constraints on the tools.

Dans ce procédé, l'outil comprend au moins deux roulettes coaxiales et séparées d'une distance correspondant à une largeur W4 d'une nervure 4. Les roulettes non représentées se déplaçent par roulement contre la face de l'ébauche de plaque. On réalise ainsi toutes les nervures 4.In this method, the tool comprises at least two coaxial wheels and separated by a distance corresponding to a width W4 of a rib 4. The unrepresented rollers move in rotation against the face of the plate blank. All the ribs 4 are thus made.

Selon un procédé de fabrication similaire, pour fabriquer l'élément d'échangeur 201, on réalise les étapes de :

  • presser et déplacer l'outil contre la face de l'ébauche de plaque, de façon à former les nervures 204 parallèles et formant des parois des canaux d'échange 206 ; et
  • presser et déplacer l'outil contre cette même face de l'ébauche de plaque, de façon à former les nervures 205 formant des parois des canaux de distribution 207.
According to a similar manufacturing method, to manufacture the exchanger element 201, the steps of:
  • pressing and moving the tool against the face of the plate blank, so as to form the parallel ribs 204 and forming walls of the exchange channels 206; and
  • pressing and moving the tool against this same face of the plate blank, so as to form the ribs 205 forming walls of the distribution channels 207.

Claims (13)

  1. Exchanger element (1; 101; 201; 301, 321, 341), for a heat exchanger (300) intended to transfer heat from at least one primary fluid, called calorigenic fluid, to at least one secondary fluid, called refrigerant, the exchanger element (1; 101; 201; 301) comprising:
    - at least one plate (2; 102; 202; 302, 322, 342) that is solid;
    - ribs (4; 104; 204; 304.1, 304.2, 324.1, 324.2, 344.1, 344.2) that protrude on at least one face of the plate (2; 102; 202; 302), each rib (4; 104; 204; 304.1) forming at least one portion of a wall of a respective channel (6; 106; 206; 306, 326, 346) suitable for the flow of calorigenic fluid or refrigerant; and
    - closing bars (8.1, 8.3; 108.1, 108.2, 108.3, 108.4; 208.1, 208.3, 208.4; 308) extending along edges of the plate (2; 102; 202; 302) in such a way as to plug at least a portion of the channels (6; 106; 206; 306);
    - the exchanger element (1-301) being characterised in that the plate (2; 102; 202; 302), at least a portion of the ribs (4; 104; 204; 304.1, 304.2, 324.1, 324.2, 344.1, 344.2) and at least a portion of the closing bars (8.1, 8.3; 108.1, 108.2, 108.3, 108.4; 208.1, 208.3, 208.4; 308) form a single piece,
    - first ribs (4) extend, protruding on at least one first face of the plate (2), in parallel in such a way as to form walls of parallel channels called exchange channels (6), ch
    aracterised in that second ribs (105; 205) are arranged protruding on the first face of the plate (102; 202) in such a way as to form walls of second channels called distribution channels (107; 207) in such a way that the distribution channels (107; 207) extend transversely to the exchange channels (106; 206).
  2. Exchanger element (1; 101; 201; 301) according to claim 1, wherein the plate (2; 102; 202; 302), all the ribs (4; 104; 204; 304.1) and all the closing bars (8.1: 308) form a single piece.
  3. Exchanger element (101; 201; 301) according to one of the previous claims,
    wherein the plate (102; 202; 302) generally has the shape of a rectangle, the exchanger element (101; 201; 301) comprising four closing bars (108.1: 308) extending along the four edges of the plate (102; 202; 302), respectively.
  4. Exchanger element (1; 101; 201) according to one of the previous claims, wherein a single face of the plate (2; 102; 202) comprises ribs (4; 104; 204).
  5. Exchanger element (301) according to one of claims 1 to 3, wherein both faces of the plate (302) comprise ribs (304.1, 304.2, 324.1, 324.2, 344.1, 344.2).
  6. Exchanger element (301) according to claim 5, wherein the ribs (304.1, 324.1, 344.1) of the first face are offset with respect to the ribs (304.2, 324.2, 344.2) of the second face, the ribs (304.1, 304.2, 324.1, 324.2, 344.1, 344.2) preferably being uniformly distributed on each face.
  7. Exchanger element (1) according to one of the previous claims, wherein each rib (4) has a width (W4) between 0.3 mm and 1.6 mm, preferably between 0.4 mm and 1.5 mm, each rib (4) has a height (H4) between 0.8 mm and 2.7 mm, preferably between 1.0 mm and 2.5 mm, wherein the plate (2) has a thickness (E2) between 0.6 mm and 1.7 mm, preferably between 0.8 mm and 1.5 mm.
  8. Exchanger element (1; 101; 201; 301) according to one of the previous claims,
    wherein the material forming the plate (2; 102; 202; 302), the ribs (4: 344.2) and the closing bars (8.1: 308) in a single piece is selected from the group consisting of copper, copper alloys, a stainless steel, aluminium, aluminium alloys, in particular grades 3003, 3004, 3104 and 3005, the plated brasing alloys 4004, 4104, 4343, 4045 and 4047A and the combination thereof with the alloys of the 3000 family.
  9. Exchanger element (1) according to one of the previous claims, wherein the distribution channels (107; 207) preferably extending at angles between 45° and 90° with respect to the exchange channels (106; 206).
  10. Exchanger element (301) according to one of claims 1 to 3 or 5 to 9, wherein:
    - the first face of the plate (302) comprises ribs (304.1) forming walls of parallel exchange channels (306); and
    - the second face of the plate (302) comprises i) ribs (304.2) forming walls of exchange channels (326) and ii) ribs forming walls of distribution channels transverse to the exchange channels (326).
  11. Heat exchanger (300) for a unit for gas separation via cryogenics, comprising a plurality of exchanger elements (301, 321, 341) comprising at least one plate (302, 322, 342) and stacked and rigidly connected to each other, for example via a brase, in such a way that the plates (302) extend in parallel to each other, the heat exchanger (300) being characterised in that said heat exchanger comprises a plurality of exchanger elements (301, 321, 341) according to one of the previous claims, preferably all the exchanger elements (301, 321, 341) are according to one of the previous claims.
  12. Heat exchanger (300) according to claim 11, wherein exchanger elements (301, 321, 341) according to claim 9 are stacked in alternation with exchanger elements (1; 101; 201; 301) according to claim 10 or 11.
  13. Manufacturing method for manufacturing an exchanger element (1; 101; 201; 301) according to one of claims 1 to 11 for a heat exchanger (300) intended to transfer heat from at least one primary fluid, called calorigenic fluid, to at least one secondary fluid, called refrigerant, the manufacturing method comprising the steps:
    - placing a mask;
    - immersing the plates in the chemical milling baths;
    - pressing and moving a tool against at least a first face of the plate blank with a pressure allowing the plate blank to be deformed plastically, in such a way as to form first parallel ribs (4: 344.2) forming walls of the exchange channels and protruding on at least one first face of a plate (2; 102; 202; 302) made from the plate blank;
    - pressing and moving the tool against said at least one first face of the plate blank in such a way as to form second ribs forming walls of the distribution channels; and
    - plastically deforming the plate blank in such a way as to form closing bars (8; 108; 208; 308) extending along edges of the plate (2; 102; 202; 302) made from the plate blank.
EP13766603.8A 2012-09-05 2013-09-02 Exchanger element for a heat exchanger, heat exchanger comprising such an exchanger element and method for the production of such an exchanger element Active EP2893278B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1258284A FR2995073A1 (en) 2012-09-05 2012-09-05 EXCHANGER ELEMENT FOR HEAT EXCHANGER, HEAT EXCHANGER COMPRISING SUCH AN EXCHANGER MEMBER, AND METHOD FOR MANUFACTURING SUCH EXCHANGER MEMBER
PCT/FR2013/052009 WO2014037656A2 (en) 2012-09-05 2013-09-02 Exchanger element for a heat exchanger, heat exchanger comprising such an exchanger element and method for the production of such an exchanger element

Publications (2)

Publication Number Publication Date
EP2893278A2 EP2893278A2 (en) 2015-07-15
EP2893278B1 true EP2893278B1 (en) 2017-02-01

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EP13766603.8A Active EP2893278B1 (en) 2012-09-05 2013-09-02 Exchanger element for a heat exchanger, heat exchanger comprising such an exchanger element and method for the production of such an exchanger element

Country Status (6)

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US (1) US10197340B2 (en)
EP (1) EP2893278B1 (en)
JP (1) JP6306018B2 (en)
CN (1) CN104769379A (en)
FR (1) FR2995073A1 (en)
WO (1) WO2014037656A2 (en)

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JP6834183B2 (en) * 2016-06-10 2021-02-24 株式会社Ihi Heat treatment equipment
FR3069918B1 (en) * 2017-08-04 2020-01-17 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude HEAT EXCHANGER COMPRISING A MULTI-CHANNEL DISTRIBUTION ELEMENT

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Also Published As

Publication number Publication date
WO2014037656A3 (en) 2015-06-11
JP2015532707A (en) 2015-11-12
FR2995073A1 (en) 2014-03-07
WO2014037656A2 (en) 2014-03-13
EP2893278A2 (en) 2015-07-15
US10197340B2 (en) 2019-02-05
JP6306018B2 (en) 2018-04-04
CN104769379A (en) 2015-07-08
US20150211809A1 (en) 2015-07-30

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